|Publication number||US6109254 A|
|Application number||US 08/946,338|
|Publication date||Aug 29, 2000|
|Filing date||Oct 7, 1997|
|Priority date||Oct 7, 1997|
|Also published as||CA2247765A1, DE69828017D1, DE69828017T2, EP0908686A2, EP0908686A3, EP0908686B1|
|Publication number||08946338, 946338, US 6109254 A, US 6109254A, US-A-6109254, US6109254 A, US6109254A|
|Inventors||Michael J. Reinke, Richard Mark DeKeuster|
|Original Assignee||Modine Manufacturing Company|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (72), Referenced by (29), Classifications (10), Legal Events (8)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This invention relates to heat exchangers, and more particularly, to clamshell heat exchangers for use in heating apparatuses such as gas fired, hot air furnaces or unit heaters.
It is known to construct the heat exchangers for gas fired, hot air furnaces from a pair of metal plates or sheets secured in face to face relationship to form a multi-pass flow passage for the hot combustion gas of the furnace. This type of heat exchanger is commonly referred to as a multi-pass clamshell heat exchanger. Typically, the multi-pass flow passage includes an inlet section an outlet section, and one or more passes connecting the inlet and outlet sections. The inlet section receives hot combustion gases from a burner, such as an inshot burner, and provides a combustion zone for the gases. The outlet section communicates with an induction draft blower or power vent which serves to draw the hot combustion gases through the multi-pass flow passage of the heat exchanger. As the combustion gas flows through the heat exchanger, it cools and becomes more dense. To maintain high gas velocity, it is known to decrease the flow area of the heat exchanger from pass to pass. It is common for a gas fired furnace to include a plurality of such clamshell heat exchangers, spaced apart in a parallel array to define air flow paths so that heat may be transferred from the hot combustion gas through the plates of the heat exchangers to the air flowing through the furnace. Examples of such clamshell heat exchangers are shown in U.S. Pat. No. 5,359,989 issued Nov. 1, 1994 to Chase et al., and U.S. Pat. No. 4,467,780 issued Aug. 28, 1984 to Ripka, the complete disclosures of which are incorporated herein by reference.
One problem commonly found in known clamshell heat exchangers are the relatively sharp angle bends that result from the formation of the hot gas combustion flow passage in the sheet metal. For example, the clamshell heat exchanger (12) in the U.S. Pat. No. 5,359,989 requires four relatively sharp angle bends for each passage (24a, 25a-c, 26a-c, and 27a-c). Such sharp angle bends produce localized material stretching that can reduce or damage anti-corrosion coatings on the surface of the material, thereby increasing the likelihood of premature corrosion failure.
Further, while many known clamshell heat exchangers perform satisfactorily, there is a continuing desire to produce more compact and efficient furnaces by decreasing the size of the heat exchangers and/or increasing the heat exchanger's performance characteristics.
It is the principal object of the invention to provide a new and improved heat exchanger, and more specifically to provide a relatively compact heat exchanger for use in heating apparatuses, such as gas fired, hot air furnaces or unit heaters, that provides improved heat transfer capabilities and/or decreases the likelihood of premature corrosion failure.
According to one facet of the invention, a clamshell heat exchanger is provided for use in a heating apparatus including a burner for producing hot combustion gas. The heat exchanger receives combustion gas from the burner and rejects heat from the combustion gas to air flowing through the furnace. The heat exchanger defines a multi-pass flow passage for the combustion gas and includes a first plate member and a second plate member. The first plate member has a first series of parallel ridges and valleys, with at least one of the valleys being deeper than other of the valleys. The second plate member faces the first plate member and includes a second series of ridges and valleys that are parallel to the first series of ridges and valleys, with at least one of the valleys of the second series being deeper than other of the valleys of the second series. A first pass of the multi-pass flow passage is defined by a number N1 of the ridges and valleys of the first and second series. A second pass of the multi-pass flow passage is defined by a number N2 of the ridges and valleys of the first and second series. The numbers N1 and N2 are different integers. The at least one deeper valley of the first series cooperates with the at least one deeper valley of the second series to separate the second pass from the first pass.
In one form, the number N2 is less than the number N1.
According to one facet of the invention, the clamshell heat exchanger includes a first plate member having a first wall section that is non-parallel to the plane of the heat exchanger, and a second plate member having a second wall section that is parallel to the first wall section and abutting the first wall section over a common length. A first pass of a multi-pass flow passage is defined by the first and second plates, and a second pass of the multi-pass flow passage is defined by the first and second plates. The second pass is parallel to the first pass and separated from the first pass by the first and second abutting wall sections.
According to one facet of the invention, the heat exchanger includes a first pass having a generally sinusoidal-shaped cross-sectional flow area, and a second pass downstream from the first pass and having a second generally sinusoidal-shaped cross-sectional flow area. The second flow area is less than the first flow area.
According to another facet of the invention, the heat exchanger includes a first planar metallic plate and a second planar metallic plate. The first planar metallic plate has at least two sections of parallel ridges displaced to one side of the plane of the first plate, valleys between the ridges, and a valley separating the sections and extending to the other side of the plane of the first plate. The second plate has at least two sections of parallel ridges displaced to the side of the second plate remote from the other side of the first plate, valleys between the ridges in the second plate, and a valley separating the sections on the second plate and extending to the side of the plane of the second plate opposite the remote side to at least nominally seal along its length with the valley separating the sections of the first plate. The ridges in the two plates are oppositely directed and generally parallel to each other to form pairs of the sections. The valleys of the second plate are nominally aligned with the ridges on the first plate. The heat exchanger further includes a combustion gas inlet to one pair of the sections, a combustion gas outlet from another pair of the sections, and a conduit formed at the interface of the plates and interconnecting the one pair of sections to said another pair of sections.
Other objects and advantages of the invention will become apparent from the following specification taken in conjunction with the accompanying drawings.
FIG. 1 is a perspective view of a clamshell heat exchanger embodying the present invention shown in combination with schematic representations of a gas inshot burner and power vent for use in a heating apparatus;
FIG. 2 is a perspective view of the opposite side of the heat exchanger shown in FIG. 1;
FIG. 3 is a cross-sectional view taken along line 3--3 in FIG. 1;
FIG. 4 is a view similar to FIG. 3, but showing an alternate embodiment of the heat exchanger; and
FIG. 5 is a schematic view of a plurality of heat exchangers embodying the present invention arranged in a parallel array in a heating apparatus.
Exemplary embodiments to the heat exchanger made according to the invention are illustrated in the drawings and described herein in connection with a heat transfer function for the hot combustion gas of a heating apparatus such as a hot air furnace or a unit heater. However, it should be understood that the invention may find utility in other applications and that no limitation to use in a gas fired, hot air furnace or unit heater is intended, except as stated in the claims.
As seen in FIGS. 1 and 2, the heat exchanger 10 includes a four pass multi-pass flow passage 11 having a J-shaped first pass or combustion gas inlet section 12, a second pass section 14, a third pass section 16, a fourth pass or combustion gas outlet section 18, a first conduit section 20 interconnecting the second and third sections 14 and 16, and a second conduit section 22 interconnecting the third section 16 and outlet section 18. As is common in gas fired furnaces, the flow passage 11 receives hot combustion gas from an inshot burner 24, and the hot combustion gas is drawn through the passage 11 by an induction draft blower or power vent 26.
As best seen in FIG. 3, the heat exchanger 10 is formed from first and second plates 30 and 32 deformed from respective planes to define the flow passage 11. Preferably, the plates 30 and 32 are formed from a suitable sheet metal and are joined at the periphery by a folded crimp 34. Each plate 30 and 32 includes a series of parallel ridges 36 and valleys 38a and 38b that define the passage sections 14, 16 and 18. The valleys 38a in each of the plates 30, 32 are deeper than the valleys 38b and cooperate with the valleys 38a of the other plate 30 and 32 to separate the second section 14 from the third section 16 and the third section 16 from the outlet section 18. More specifically, each of the valleys 38a includes a wall section 40 that is non-parallel to the plane of the heat exchanger and that abuts a parallel wall section 40 of a corresponding valley 38a over a common length to separate the passage sections 14, 16 and 18. Preferably, each of the abutting wall sections 40 have a width W that is sufficient for the valleys 38a to be at least nominally sealed along the common length of the abutting wall sections 40.
The inlet section 12 is separated from the second section 14 by wall sections 42 and 44 provided on the first and second plates 30 and 32, respectively. The wall sections 42 and 44 are parallel with and lie in the plane of their respective plates 30 and 32. Preferably, the wall sections 42 and 44 are at least nominally sealed over their common length.
It should be appreciated that there must be a transition between the wall sections 40, which are nonparallel to the plane of the heat exchanger 10, and the periphery 45 of the plates 30, 32 which is parallel to the plane of the heat exchanger. As best seen in FIGS. 1 and 2, these transitions occur in a zone 46 between the second section 14 and the third section 16, and in a zone 47 between the third section 16 and the gas outlet section 18, as best seen in FIG. 2. Thus, the shape of each plate 30 and 32 extends parallel to the plane of the heat exchanger 10 into each of the transition zones 46 and 47 and changes gradually to the angle of the nonplanar wall section 40 between the periphery 45 and the beginning of each of the passage sections 14, 16. In this manner, the largest possible seal is maintained throughout each of the transition zones 46 and 47.
In a highly preferred embodiment, the wall sections 40 and the wall sections 42 and 44 are joined together with clinch holes or buttons, or staked together with a TOX® joint using tooling provided by Pressotechnik, Inc., 730 Racquet Club Drive, Addison, Ill. 60101.
As seen in FIG. 3, the second section 14 has a sinusoidal-shaped flow area 50 defined by two of the ridges 36, two of the valleys 38b and one of the valleys 38a in the first plate 30 and two of the ridges 36 and two of the valleys 38b in the second plate 32. The third section 16 has a sinusoidal-shaped flow area 52 defined by two of the ridges 36 and one of the valleys 38b in the first plate 30 and one of the ridges 36 and two of the valleys 38a in the second plate 32. The outlet section 18 has a sinusoidal-shaped flow area 54 defined by one of the ridges 36, one of the valleys 38a and one of the valleys 38b of the first plate 30 and one of the ridges 36 and one of the valleys 38b of the second plate 32. Thus, the second section 14 is defined by nine of the ridges 36 and valleys 38a-b; the third section 16 is defined by six of the ridges 36 and valleys 38a-b; and the outlet section 18 is defined by five of the ridges 36 and valleys 38a-b. Accordingly, the flow area 50 of the second section 14 is greater than the flow area 52 of the third section 16, and the flow area 52 of the third section 16 is greater than the flow area 54 of the outlet section 18.
FIG. 4 shows another embodiment of the heat exchanger 10 that is identical to the embodiment shown in FIG. 3, with the exception that each of the plates 30 and 32 has an additional valley 38a that replaces the wall sections 42 and 44, a valley 38b in the plate 30 and a valley 38b in the plate 32. This allows the embodiment in FIG. 4 to have a shorter length L than the embodiment in FIG. 3.
As best seen in FIG. 5, a plurality of the heat exchangers 10 can be arranged in a parallel array in a furnace or unit heater 50 to define a plurality of continuous, sinusoidal flow paths 52 for the air flowing through the furnace across the exterior of the heat exchangers 10. It should be understood that the heat exchangers 10 may be installed in the furnace or unit heater 50 so that air flows through the flow paths 52 in either the direction shown by arrows A or the direction shown by arrows B. Further, it should be appreciated that the heat exchangers 10 may be arranged in the furnace or unit heater 50 with the planes of the heat exchangers 10 extending vertically and the air flow moving vertically in the flow paths 52, or with the planes of the heat exchangers 10 extending horizontally and the air flow moving horizontally in the flow paths 52.
In operation, hot combustion gas is directed into the inlet section 12 by the inshot burner 24 and continues to combust as it passes through the inlet section 12. The power vent 26 provides an induction draft which induces the hot combustion gases from the burner 24 to flow through the passage sections 12, 14, 16 and 18. The stepwise area reduction of the flow areas 50, 52 and 54 maintains a high gas velocity for the combustion gases as they flow through the passage 11.
It should be appreciated that the gentle sinusoidal shape of the plates 30 and 32 minimizes the number of sharp angles in the heat exchanger 10, thereby reducing the likelihood of premature corrosion failure resulting from damage to anticorrosion coatings on the surface of the plates 30 and 32 during forming operations.
It should also be appreciated that the sinusoidal shape of the flow areas 50, 52 and 54 allows for an increased heat transfer surface area per unit volume while providing a relatively small hydraulic diameter and a relatively large wetted perimeter, thereby increasing heat transfer performance. Further, the passage shapes induce turbulence in the air flowing about the exterior of the heat exchanger.
It should further be appreciated that by separating the passage sections 12, 14, 16 and 18 with wall sections 40 that are non-parallel to the plane of the plates 30 and 32, the overall length L of the heat exchangers 10 can be reduced while still providing a width of contact area W between the sections that is adequate to at least nominally seal adjacent sections and to allow for an adequate structural connection.
It should also be appreciated that the peaks 36 and valleys 38a-bstiffen the plates 30 and 32 along the length of each of the passage sections 14, 16 and 18, thereby reducing undesirable deformation of the passage sections 14, 16 and 18 resulting from thermal induced stresses.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2751900 *||May 22, 1951||Jun 26, 1956||Modine Mfg Co||Combustion type heater|
|US3661140 *||Jun 17, 1970||May 9, 1972||Carrier Corp||Gas-fired furnace|
|US4154213 *||May 2, 1977||May 15, 1979||The Coleman Company, Inc.||Ductless forced-circulation undercounter furnace|
|US4298061 *||Aug 15, 1980||Nov 3, 1981||The Singer Company||Heat exchanger with crimped flange seam|
|US4467780 *||May 17, 1982||Aug 28, 1984||Carrier Corporation||High efficiency clamshell heat exchanger|
|US4476850 *||Sep 2, 1982||Oct 16, 1984||Carrier Corporation||Noise reducing heat exchanger assembly for a combustion system|
|US4510660 *||Sep 13, 1982||Apr 16, 1985||Snyder General Corporation||Method of manufacturing a two-plate heat exchanger|
|US4538338 *||May 2, 1983||Sep 3, 1985||Snyder General Corporation||Method for manufacturing a furnace heat exchanger and plate assembly|
|US4547943 *||Dec 11, 1981||Oct 22, 1985||Snyder General Corporation||Method of manufacturing a heat exchanger and plate assembly|
|US4570612 *||Nov 19, 1984||Feb 18, 1986||Carrier Corporation||Induced draft submerged burner|
|US4730600 *||Dec 16, 1981||Mar 15, 1988||The Coleman Company, Inc.||Condensing furnace|
|US4739746 *||Oct 23, 1986||Apr 26, 1988||Heil-Quaker Home Systems, Inc.||Heat exchanger for furnace|
|US4779676 *||Jun 5, 1986||Oct 25, 1988||The Coleman Company, Inc.||Condensing furnace|
|US4848314 *||Nov 27, 1987||Jul 18, 1989||Carrier Corporation||Condensing furnace|
|US4867673 *||Jul 27, 1988||Sep 19, 1989||The Coleman Company, Inc.||Condensing furnace|
|US4877014 *||Jan 19, 1988||Oct 31, 1989||American Standard Inc.||Tube arrangement for heat exchanger|
|US4887959 *||Nov 17, 1988||Dec 19, 1989||Rheem Manufacturing Company||Gas furnace with improved ignition|
|US4893390 *||Sep 1, 1988||Jan 16, 1990||Snyder General Corporation||Method and expander for manufacturing a furnace heat exchanger and plate assembly|
|US4924848 *||Aug 21, 1989||May 15, 1990||Nordyne, Inc.||High-efficiency furnace for mobile homes|
|US4945890 *||Sep 5, 1989||Aug 7, 1990||Carrier Corporation||Induced draft warm air furnace with radiant infrared burner|
|US4955359 *||Aug 8, 1989||Sep 11, 1990||Robert Sun Company||Furnace with counterflow heat exchange means|
|US4960102 *||Feb 5, 1990||Oct 2, 1990||Rheem Manufacturing Company||Fuel-fired condensing type forced air heating furnace|
|US4974579 *||Sep 28, 1989||Dec 4, 1990||Rheem Manufacturing Company||Induced draft, fuel-fired furnace apparatus having an improved, high efficiency heat exchanger|
|US4982785 *||Mar 6, 1990||Jan 8, 1991||Inter-City Products Corporation (Usa)||Serpentine heat exchanger|
|US4987881 *||Mar 16, 1990||Jan 29, 1991||Narang Rajendra K||Fuel burning furnace|
|US5042453 *||Jul 27, 1990||Aug 27, 1991||Rheem Manufacturing Company||Compact, high efficiency heat exchanger for a fuel-fired forced air heating furnace|
|US5052345 *||Oct 12, 1989||Oct 1, 1991||Kurt Bystrom||Heating apparatus with a heat exchanger|
|US5060722 *||Nov 6, 1990||Oct 29, 1991||American Standard, Inc.||Furnace heat exchanger|
|US5062409 *||Apr 16, 1990||Nov 5, 1991||Nepon Company, Ltd||Hot-air furnace|
|US5065736 *||Feb 1, 1991||Nov 19, 1991||Engineered Air Systems, Inc.||Air heating apparatus and method of heating an air stream|
|US5074280 *||Mar 13, 1991||Dec 24, 1991||Lennox Industries Inc.||Sectional high efficiency heat exchanger|
|US5094224 *||Feb 26, 1991||Mar 10, 1992||Inter-City Products Corporation (Usa)||Enhanced tubular heat exchanger|
|US5097802 *||Nov 30, 1990||Mar 24, 1992||Raytheon Company||Condensing furnace with submerged combustion|
|US5105798 *||Aug 6, 1991||Apr 21, 1992||Lennox Industries Inc.||Heating efficiency and noise reduction enclosure|
|US5113844 *||Dec 12, 1989||May 19, 1992||Vulcan Australia Limited||Heat exchanger|
|US5141152 *||Dec 21, 1990||Aug 25, 1992||York International||Flue gas closure system|
|US5142895 *||May 15, 1989||Sep 1, 1992||Amana Refrigeration, Inc.||Method for bending tubes|
|US5146910 *||Jul 18, 1991||Sep 15, 1992||Rheem Manufacturing Company||NOX reducing device for fuel-fired heating appliances|
|US5165386 *||Oct 1, 1991||Nov 24, 1992||Veg-Gasinstituut N.V.||Compact gas-fired air heater|
|US5176512 *||Mar 13, 1991||Jan 5, 1993||Lennox Industries Inc.||Inshot burner cluster apparatus|
|US5195580 *||Feb 11, 1992||Mar 23, 1993||Ehrhardt Tool And Machine Co., Inc.||Heat exchanger seam and method of making same|
|US5201651 *||Mar 11, 1991||Apr 13, 1993||T.A. Pelsue Company||Construction heater and method of manufacture of heater|
|US5205276 *||Nov 21, 1991||Apr 27, 1993||Gas Research Institute||Compact furnace heat exchanger|
|US5222552 *||Jun 3, 1992||Jun 29, 1993||Amana Refrigeration, Inc.||Tubular heat exchanger and method for bending tubes|
|US5271376 *||Apr 2, 1993||Dec 21, 1993||Rheem Manufacturing Company||Serpentined tubular heat exchanger apparatus for a fuel-fired forced air heating furnace|
|US5284041 *||May 10, 1993||Feb 8, 1994||Amana Refrigeration, Inc.||Method for bending tubes using split die|
|US5295473 *||Mar 18, 1992||Mar 22, 1994||Neufeldt Jacob J||Furnace|
|US5301654 *||Jul 29, 1992||Apr 12, 1994||Consolidated Industries Corp.||Heat-exchanger especially for forced air furnaces|
|US5309890 *||Jul 30, 1993||May 10, 1994||Carrier Corporation||Dual-sided condensate trap for furnace|
|US5309892 *||Aug 27, 1992||May 10, 1994||American Standard Inc.||Blower deck for upflow or downflow furnace|
|US5322050 *||Jul 21, 1993||Jun 21, 1994||Rheem Manufacturing Company||High efficiency fuel-fired condensing furnace having a compact heat exchanger system|
|US5333597 *||Apr 30, 1993||Aug 2, 1994||Consolidated Industries Corp.||Abatement member and method for inhibiting formation of oxides of nitrogen|
|US5345924 *||Jul 2, 1993||Sep 13, 1994||Carrier Corporation||Cold spot baffle for coupling box|
|US5346001 *||Jul 7, 1993||Sep 13, 1994||Carrier Corporation||Primary heat exchanger having improved heat transfer and condensate drainage|
|US5346002 *||Sep 9, 1993||Sep 13, 1994||Carrier Corporation||Cell panel with extruded burner target plates and process for making same|
|US5359989 *||Mar 4, 1993||Nov 1, 1994||Evcon Industries, Inc.||Furnace with heat exchanger|
|US5368010 *||Jul 29, 1992||Nov 29, 1994||Consolidated Industries Corp.||Multi-position forced air furnace|
|US5368011 *||Jun 9, 1993||Nov 29, 1994||Rheem Manufacturing Company, A Delaware Corp.||Appliance combustion chamber|
|US5368012 *||Feb 7, 1994||Nov 29, 1994||Williams Furnace Company||Wall furnace with side vented draft hood|
|US5370529 *||Aug 24, 1993||Dec 6, 1994||Rheem Manufacturing Company||Low NOx combustion system for fuel-fired heating appliances|
|US5375586 *||Aug 11, 1993||Dec 27, 1994||Inter-City Products Corporation (Usa)||Condensate isolator and drainage system for furnace|
|US5379750 *||Sep 16, 1993||Jan 10, 1995||Carrier Corporation||Burner mounting assembly for gas furnace|
|US5379751 *||Dec 20, 1993||Jan 10, 1995||Carrier Corporation||Inducer collector box seal for induction condenser furnace|
|US5380193 *||Dec 2, 1993||Jan 10, 1995||Carrier Corporation||Apparatus for attaching manifold assembly to gas control assembly of furnace|
|US5402567 *||Aug 2, 1994||Apr 4, 1995||Robertshaw Controls Company||Method of making a jet burner construction|
|US5406933 *||Mar 16, 1994||Apr 18, 1995||Rheem Manufacturing Company||High efficiency fuel-fired condensing furnace having a compact heat exchanger system|
|US5406934 *||Mar 23, 1993||Apr 18, 1995||Cain Industries, Inc.||Heat recovery apparatus for use with a non-high efficiency furnace|
|US5417199 *||Nov 2, 1993||May 23, 1995||Lennox Industries Inc.||Heating apparatus convertible for upflow or downflow operation|
|US5437263 *||Aug 27, 1993||Aug 1, 1995||Goodman Manufacturing Company||High efficiency furnace method and apparatus|
|US5448986 *||Jul 21, 1993||Sep 12, 1995||Lennox Industries Inc.||Heat exchanger|
|AU537408A *||Title not available|
|DK42553A *||Title not available|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US6422306||May 9, 2001||Jul 23, 2002||International Comfort Products Corporation||Heat exchanger with enhancements|
|US6470878 *||Oct 23, 2000||Oct 29, 2002||Carrier Corporation||Furnace heat exchanger|
|US6484798||Oct 23, 2000||Nov 26, 2002||Carrier Corporation||Furnace heat exchanger|
|US6764761||May 24, 2002||Jul 20, 2004||Baxter International Inc.||Membrane material for automated dialysis system|
|US6793015 *||Oct 23, 2000||Sep 21, 2004||Carrier Corporation||Furnace heat exchanger|
|US6869538||May 24, 2002||Mar 22, 2005||Baxter International, Inc.||Method and apparatus for controlling a medical fluid heater|
|US6938688||Nov 19, 2002||Sep 6, 2005||Thomas & Betts International, Inc.||Compact high efficiency clam shell heat exchanger|
|US7096933||Oct 24, 2000||Aug 29, 2006||Carrier Corporation||Furnace heat exchanger|
|US7175606||May 24, 2002||Feb 13, 2007||Baxter International Inc.||Disposable medical fluid unit having rigid frame|
|US7731689 *||Feb 15, 2007||Jun 8, 2010||Baxter International Inc.||Dialysis system having inductive heating|
|US7789849||Sep 7, 2010||Baxter International Inc.||Automated dialysis pumping system using stepper motor|
|US7809254||Jul 5, 2007||Oct 5, 2010||Baxter International Inc.||Dialysis fluid heating using pressure and vacuum|
|US7815595||Oct 19, 2010||Baxter International Inc.||Automated dialysis pumping system|
|US8078333||Dec 13, 2011||Baxter International Inc.||Dialysis fluid heating algorithms|
|US8206338||Jun 26, 2012||Baxter International Inc.||Pumping systems for cassette-based dialysis|
|US8403880||Mar 26, 2013||Baxter International Inc.||Peritoneal dialysis machine with variable voltage input control scheme|
|US8529496||Jun 9, 2010||Sep 10, 2013||Baxter International Inc.||Peritoneal dialysis machine touch screen user interface|
|US8803044||Jul 5, 2007||Aug 12, 2014||Baxter International Inc.||Dialysis fluid heating systems|
|US8826901||Jan 20, 2011||Sep 9, 2014||Carrier Corporation||Primary heat exchanger design for condensing gas furnace|
|US20030102115 *||Nov 19, 2002||Jun 5, 2003||Thomas & Betts International, Inc.||Compact high efficiency clam shell heat exchanger|
|US20030217957 *||May 24, 2002||Nov 27, 2003||Bowman Joseph H.||Heat seal interface for a disposable medical fluid unit|
|US20030217975 *||May 24, 2002||Nov 27, 2003||Yu Alex Anping||Method and apparatus for controlling a medical fluid heater|
|US20080021377 *||Jul 5, 2007||Jan 24, 2008||Baxter International Inc.||Dialysis fluid heating systems|
|US20080200866 *||Feb 15, 2007||Aug 21, 2008||Baxter International Inc.||Dialysis system having inductive heating|
|US20090010627 *||Jul 5, 2007||Jan 8, 2009||Baxter International Inc.||Dialysis fluid heating using pressure and vacuum|
|US20090183862 *||Jan 12, 2005||Jul 23, 2009||Sylvain Benezech||Heat exchanger and related exchange module|
|US20110174299 *||Jul 21, 2011||Lennox Industries, Incorporated||Heat exchanger having an interference rib|
|US20110174301 *||Jul 21, 2011||Carrier Corporation||Primary Heat Exchanger Design for Condensing Gas Furnace|
|US20110174302 *||Jul 12, 2010||Jul 21, 2011||Lennox Industries Inc.||Heat exchanger expanded overlap joint|
|U.S. Classification||126/110.00R, 126/99.00R, 165/170, 165/147|
|International Classification||F24H3/10, F28D9/00|
|Cooperative Classification||F24H3/105, F28D9/0031|
|European Classification||F24H3/10C, F28D9/00F|
|Aug 21, 1998||AS||Assignment|
Owner name: MODINE MANUFACTURING COMPANY, WISCONSIN
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:REINKE, MICHAEL J.;DEKEUSTER, RICHARD MARK;REEL/FRAME:009404/0282
Effective date: 19970929
|Mar 1, 2004||FPAY||Fee payment|
Year of fee payment: 4
|Feb 28, 2008||FPAY||Fee payment|
Year of fee payment: 8
|Mar 10, 2008||REMI||Maintenance fee reminder mailed|
|Feb 18, 2009||AS||Assignment|
Owner name: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT, NE
Free format text: SECURITY AGREEMENT;ASSIGNORS:MODINE MANUFACTURING COMPANY;MODINE, INC.;MODINE ECD, INC.;REEL/FRAME:022266/0552
Effective date: 20090217
|Apr 9, 2012||REMI||Maintenance fee reminder mailed|
|Aug 29, 2012||LAPS||Lapse for failure to pay maintenance fees|
|Oct 16, 2012||FP||Expired due to failure to pay maintenance fee|
Effective date: 20120829